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A compressor is used to bring saturated water vapor at 103 lbf/in.2 up to 2000 lbf/in.2, where the actual exit temperature is 1200 F. Find the isentropic compressor efficiency and the entropy generation. 

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C.V. Compressor. Assume adiabatic and neglect kinetic energies

Energy Eq.  w = h1 - h2

Entropy Eq  s2 = s1 + sgen

We have two different cases, the ideal and the actual compressor.

States: 1: h1 = 1188.36 Btu/lbm, s1 = 1.601 Btu/lbm R

2ac:  h2,AC = 1598.6 Btu/lbm, s2,AC = 1.6398 Btu/lbm R

2s: F.7.2 (P, s = s1) h2,s = 1535.1 Btu/lbm 

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